US10456742B2ActiveUtilityA1

Aqueous lime slurry, preparation process and uses

Assignee: COATEX SASPriority: Nov 19, 2012Filed: Feb 23, 2017Granted: Oct 29, 2019
Est. expiryNov 19, 2032(~6.3 yrs left)· nominal 20-yr term from priority
B01D 2251/404B01D 53/502B01D 53/68B01D 53/64C01F 11/02B01D 53/1493B01F 3/0811B01D 53/48C02F 11/14B01F 23/4105C02F 11/148
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14
Claims

Abstract

Preparation of aqueous slurries of calcium dihydroxide. Preparation of aqueous suspensions of calcium hydroxide.

Claims

exact text as granted — not AI-modified
The invention claimed is: 
     
       1. An aqueous slurry of calcium hydroxide comprising water, calcium hydroxide, and a copolymer, said slurry having a dry content of at least 40% by weight, the viscosity of said aqueous slurry as measured by a Brookfield DVIII viscometer at 10 RPM being between 25 and 1,000 mPa·s at 20° C.,
 wherein said copolymer consists: 
 of methacrylic acid monomers and/or any of its salts, 
 optionally of acrylic acid monomers and/or any of its salts, 
 of one or more monomers with the formula (I):
   R—X—R′  (I)
 
 
 where: 
 R represents a polymerizable unsaturated group, 
 R′ represents hydrogen or an alkyl group with from 1 to 4 carbon atoms, 
 X represents a structure with n unit(s) of ethylene oxide EO and m unit(s) of propylene oxide PO, arranged randomly or regularly, and 
 m and n are independent non-zero integers and are between 1 and 150, and wherein said slurry is prepared by a process comprising: 
 agitating a mixture of the water and the copolymer to form an aqueous solution; 
 adding the calcium hydroxide in powdered form to said aqueous solution and agitating to provide an initial slurry; 
 applying a homogeneous shear level greater than 50,000 s −1  to the initial slurry; and 
 optionally, while applying said shear level to said initial slurry, adding more copolymer and/or more powdered calcium hydroxide to said initial slurry. 
 
     
     
       2. The aqueous slurry according to  claim 1 , wherein the copolymer has a molecular mass between 30,000 and 200,000 g/mol as determined by Gel Permeation Chromatography (GPC). 
     
     
       3. The aqueous slurry according to  claim 1 , wherein the monomer of formula (I) is such that n+m>17. 
     
     
       4. The aqueous slurry according to  claim 1 , wherein the R group of said monomer of formula (I) represents the methacrylate group. 
     
     
       5. The aqueous slurry according to  claim 1 , wherein the R′ group of the monomer of formula (I) represents H or CH 3 . 
     
     
       6. The aqueous slurry according to  claim 1 , wherein the monomer of formula (I) consists of, expressed as a percentage by weight of each of its components:
 5 to 30% by weight of methacrylic acid monomers and/or any of its salts, 
 0 to 10% by weight of acrylic acid monomers and/or any of its salts, 
 70 to 95% by weight of monomers of formula (I). 
 
     
     
       7. The aqueous slurry according to  claim 1 , wherein a mixer of the rotor-stator type is used to apply said shear. 
     
     
       8. The aqueous slurry according to  claim 1 , wherein the shear is applied in a device equipped with a recirculating loop. 
     
     
       9. The aqueous slurry according to  claim 1 , wherein the shear is applied in a device configured to deliver an output of at least 1,000 W/m 3 . 
     
     
       10. The aqueous slurry according to  claim 1 , wherein the R group of said monomer of formula (I) represents an acrylate, methacrylate, methacrylurethane, vinyl or allyl group. 
     
     
       11. A method of treating industrial smoke, domestic wastewater, or industrial wastewater, comprising contacting said smoke or wastewater with the aqueous slurry according to  claim 1 . 
     
     
       12. A method of flue gas desulfurization, comprising contacting industrial smoke with the aqueous slurry according to  claim 1 . 
     
     
       13. A process for the preparation of the aqueous slurry of calcium hydroxide of  claim 1 , the process comprising:
 agitating a mixture of the water and the copolymer to form an aqueous solution; 
 adding the calcium hydroxide in powdered form to said aqueous solution and agitating to provide an initial slurry; 
 applying a homogeneous shear level greater than 50,000 s −1  to the initial slurry; and 
 optionally, while applying said shear level to said initial slurry, adding more copolymer and/or more powdered calcium hydroxide to said initial slurry. 
 
     
     
       14. A process according to  claim 13 , wherein said process comprises adding more copolymer and/or more powdered calcium hydroxide to said initial slurry while applying said shear level to said initial slurry.

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